2-Hydroxymethyl-1,3-propanediol preparation

ABSTRACT

2-Hydroxymethyl-1,3-propanediol trinitrate, processes for its preparation, and compounds related thereto are disclosed. The final product is useful as a plasticizer of relatively low volatility in double based propellant compositions and as a liquid explosive.

This is a divisional, of application Ser. No. 854,946 filed Nov. 25, 1977, now abandoned.

BACKGROUND OF THE INVENTION

Double base and crosslinked double base propellants are well-known as high energy propellants. These propellants employ nitroglycerin as a plasticizer.

Nitroglycerin has a number of undesirable qualities which limits the usefulness of propellants employing it. The principal deficiencies are:

(1) Marginal thermal stability coupled with auto catalysis of the decomposition by the decomposition products requiring elaborate stabilization systems to provide adequate shelf life;

(2) Difficulty in achieving high solids loading;

(3) Difficulty in achieving good mechanical properties by using HMX coating agents; and

(4) A relatively high vapor pressure causing exudation during vacuum processing, and migration over long periods at ambient temperatures and pressures.

The present invention relates to a novel compound 2-hydroxymethyl-1,3-propanediol trinitrate and its use in replacing nitroglycerin in double base propellants to ameliorate the problems associated with the use of nitroglycerin.

The invention also provides novel processes for the preparation of 2-hydroxymethyl-1,3-propanediol which enable the preparation of this compound in significantly greater yield than those afforded by procedures of the prior art.

DISCUSSION OF THE PRIOR ART

The following references, copies of which accompany this application, are considered to have some relevance to the invention of this application.

Breusch and Oguzer in Chemische Berichte, Volumn 88, page 1511 (1955) reported a synthesis of 2-hydroxymethyl-1,3-propanediol (trimethylol methane) by lithium aluminum hydride reduction of methane tricarboxylic acid triethylester. They reported a 5% yield of a solid melting at 59°-62° C.

Boros et al in The Journal of the American Chemical Society, Volume 88, page 1140 (1966) reported a modification of the earlier synthesis of trimethylol methane. They reported in 18% yield of a low-melting solid.

Seiiti Fujii in Review of Physical Chemistry of Japan, Volume 20, page 153 (1946) discusses the products of hydrogenation of the condensation products of acetone and formaldehyde. He obtains one high melting product, which he names tetraglycerol, of melting point 178° C. and to which he assigns the structure (HOCH₂)₃ CH. He also reports a trinitrate of this compound having a melting point of 137° C. The so-called tetraglycerol was identified by an "ultimate analysis" whose results are not reported. Based on the results later found by Breusch and Oguzer and by Boros et al as well as the data reported in this application which is consistent with their findings, whatever compound Fujii had, it was not trimethyol methane and hence he could not have prepard trimethylol methane trinitrate.

SUMMARY OF THE INVENTION

The invention provides in a composition aspect a compound which is 2-hydroxymethyl-1,3-propanediol trinitrate.

The tangible embodiment of this composition aspect of the invention possesses the inherent physical properties of being a water white liquid at ordinary room temperature, being relatively non-volatile, being substantially insoluble in water and carbon tetrachloride but soluble in such organic solvents as lower alkanols e.g. methanol, ethanol; ketones, e.g. acetone, ethyl methyl ketone; esters, e.g. ethyl acetate; and such other common solvents as dimethyl sulfoxide, acetonitrile and dimethyl formamide.

Examination of the product produced by the hereinafter described processes reveals upon, nuclear magnetic resonance, and infrared spectral analysis, spectral data supporting the herein named structure.

The tangible embodiment of the composition aspect of the invention possesses the inherent applied use characteristic of being a plasticizer for double based propellants.

The invention further provides in another composition aspect a propellant composition comprising an oxidizer component, a binder component and 2-hydroxymethyl-1,3-propanediol trinitrate.

The tangible embodiments of this composition aspect of the invention possess the inherent applied use characteristics of being energetic propellants while being more storage and processing stable than comparable propellants containing nitroglycerin in place of 2-hydroxymethyl-1,3-propanediol trinitrate.

The invention further provides in a process aspect a process for the preparation of 2-hydroxymethyl-1,3-propanediol which comprises the treatment of bis-(hydroxymethyl) acetaldehyde with an aldehyde carbonyl group reducing agent selected from hydrogen absorbed on a platinum, rhodium, or palladium hydrogenation catalyst, or an alkali metal dissolving in a lower alkanol.

Special mention is made of aspects of this process wherein the reducing agent is hydrogen adsorbed on a platinum catalyst or is sodium dissolving in ethanol.

The invention further provides a process for the preparation of 2-hydroxymethyl-1,3-propanediol which comprises:

(a) treating a compound of the formula: ##STR1## wherein the R moieties are the same or different and are lower alkyl, with a hydroxyl group protecting reagent, to produce a compound of the formula: ##STR2## wherein X represents the protected hydroxyl groups and R is defined hereinabove;

(b) treating the product of step a with an ester group hydrolysis reagent so as to produce a compound of the formula: ##STR3## wherein X and R are as defined hereinabove;

(c) treating the product of step b with an ester group reducing agent selected from hydrogen adsorbed on a catalyst, aluminum hydrides, borohydrides, borane-dimethyl sulfide, or an alkali metal dissolving in a lower alkanol to give a product of the formula: ##STR4## wherein X is as defined hereinabove; and

(d) removing the hydroxyl protecting groups from the product of step c.

The invention further provides in a process aspect a process for the preparation of 2-hydroxymethyl-1,3-propanediol which comprises treating a compound of the formula: ##STR5## wherein the R' moieties are the same or different and are lower alkyl, with an adduct of borane and dimethyl sulfide.

The invention further provides a process for the preparation of 2-hydroxymethyl-1,3-propanediol trinitrate which comprises:

(a) preparing 2-hydroxylmethyl-1,3-propanediol by any of the herein described processes or by the methods of the hereinabove mentioned processes of Breusch and Oguzer and Boros et al; and

(b) treating the product of step a with nitric acid in a substantially non-aqueous medium in the presence of a water absorber.

The invention also provides in a process aspect a process for inducing peripheral vasodilation in a warm blooded animal which comprises administering to a warm blooded animal, in need thereof, an effective amount of a comound of the formula:

    R--C(CH.sub.2 ONO.sub.2).sub.3 ps

wherein R is hydrogen, methyl, or ethyl.

Special mention is made of the embodiment of this process wherein R is hydrogen.

DESCRIPTION OF THE PREFERRED EMBODIMENT

The preparation of the compositions of the invention may be performed by several processes.

2-Hydroxymethyl-1,3-propanediol trinitrate may be prepared by treating 2-hydroxymethyl-1,3-propanediol with excess nitric acid, conveniently anhydrous nitric acid, in the presence of a water absorber, conveniently fuming sulfuric acid, at below normal ambient temperature, conveniently 10°-15° C., conveniently in the presence of an immiscible solvent, conveniently methylene chloride, conveniently, but not essentially, while monitoring the redox potential of the system, while stirring. The immiscible solvent serves the convenient purpose of removing the nitrate ester from the acid phase as it is formed. Combination of reactants is conveniently accomplished by incremental addition of the alcohol to the acid. When the addition is complete, the reaction is essentially complete and the product may be removed by standard means. Separation of the phases, if the treatment has been performed in a 2 phase system, or the addition of a suitable immiscible solvent followed by separation of the organic phase permits recovery of 2-hydroxymethyl-1,3-propanediol trinitrate from the organic phase by standard techniques. If desired, recovery may be accomplished by neutralization of any acidity present in the organic phase, drying and evaporation of the solvent.

Propellant compositions may be prepared by using 2-hydroxymethyl-1,3-propanediol trinitrate in place of nitroglycerin in standard double base propellants.

The same standard processing techniques, as well as, standard propellant binders, oxidizers, and optionally the usual metal fuels, various adjuvants and cure and combustion catalysts and additional standard plasticizers may be employed as desired by the compounder.

2-Hydroxymethyl-1,3-propanediol may be prepared by a number of alternative procedures from known starting materials.

Bis-(hydroxymethyl) acetaldehyde may be treated in solution, conveniently aqueous solution, with hydrogen in the presence of a catalyst, conveniently at low to moderate pressures, 35 to 600 psi, preferably 50 to 500 psi using platinum, palladium or rhodium catalysts, preferably platinum, until a stoichiometric quantity of hydrogen is absorbed. Separation of the catalyst, followed by removal of the solvent is convenient method of recovering 2-hydroxymethyl-1,3-propanediol. It will be readily apparent to one skilled in the art that alternative means of reducing the aldehyde carbonyl group may be employed. An alkali metal, conveniently sodium, dissolving in a lower alkanol, conveniently ethanol (Bouveault Blanc reduction) is a convenient method.

Commercially available diethyl-bis(hydroxymethyl) malonate may be treated with a hydroxyl group protecting agent, conveniently acetone, in an inert water immiscible solvent, conveniently benzene, in the presence of an acid catalyst, conveniently phosphoric acid, at elevated temperature, conveniently the reflux temperature of the solvent employed, while separating the water which azeotropes with the solvent. If desired, when the theoretical quantity of water has been recovered the hydroxyl group protected product, in the case of acetone, 2,2-dimethyl-5,5-dicarbethoxy- 1,3-dioxane, may be recovered by standard techniques. Separation and neutralization of the organic phase of the reaction mixture followed by evaporation of the inert solvent and any remaining hydroxyl group protecting agent is a convenient method. The hydroxyl protected product so produced may then be subjected to partial ester hydrolysis which will result in decarboxylation of the resultant β-carboxylic acid ester. Treatment in dimethyl sulfoxide in the presence of sodium chloride at elevated temperature, conveniently between 150° and 200° C., preferably between 170° and 180° C., with water while distilling water and ethanol is a convenient hydrolysis procedure. When the theoretical amount of ethanol has been recovered, the mixture may be cooled, partitioned between water and an immiscible solvent, conveniently ether, followed by separation and drying of the organic layer, evaporation of solvent and distillation of the hydroxyl protected, decarboxylated product, which if acetone is the protecting group will be 2,2-dimethyl-5-carbethoxy-1,3-dioxane.

This product may then be treated with an ester group reducing agent, conveniently lithium aluminum hydride, in a suitable solvent, conveniently ether, tetrahydrofuran or a mixture of ether and tetrahydrofuran, at ambient temperature. When the carboxyl function has been reduced the mixture may be decomposed with water, the solids removed by filtration and solvents evaporated to give the reduced hydroxyl protected product, which if acetone was the original protecting group will be 2,2-dimethyl-5-hydroxymethyl-1,3-dioxane. If desired the product may be purified by distillation in vacuo.

The protecting group may then be removed from the protected product by treatment with an appropriate hydrolytic system. If acetone was the original protecting group, treatment with aqueous hydrochloric acid at ambient temperature is a convenient method. The product, 2-hydroxymethyl-1,3-propanediol may be recovered by standard techniques. Evaporation of the hydrolysis mixture followed by recrystallization of the residual solid from acetone is a convenient method.

Tricarbo lower alkoxy methanes, available from di lower alkyl malonic esters by treatment with magnesium followed by lower alkyl chloroformates, may be treated with a borane-dimethyl sulfide adduct. After reduction of the carboxyl groups is complete, the reaction mixture may be decomposed with water, the resulting mixture partitioned between ether and water, the organic phase dried and solvent evaporated and the residue distilled to give 2-hydroxymethyl-1,3-propanediol.

The starting materials for the practice of the invention namely bis-(hydroxymethyl) acetaldehyde, di lower alkyl bis-(hydroxymethyl) malonate and tricarbo lower alkoxy methane are all commercially available or readily preparable by standard synthetic methods well-known in the literature. The preparation of bis-(hydroxymethyl) acetaldehyde is described by Vik in Acta Chimica Scandinavica, Vol. 27, page 239 (1973). Diethyl bis-(hydroxymethyl) malonate may be synthesized by a procedure described in Org. Synth. Vol. 40, page 27. The preparation of other lower alkyl esters by analogous methods will be obvious to one of average skill in the art. The general procedure for the synthesis of tricarbo lower alkoxy methanes has been outlined hereinabove. The borane-dimethyl sulfide adduct is commercially available.

In the process for the use of the compounds of the formula

    R--C(CH.sub.2 ONO.sub.2).sub.3

wherein R is as defined hereinabove, they may, if desired, be formulated with pharmaceutically acceptable carriers in accordance with methods well-known in the art. The peripheral vasodilation activity of these compounds may be demonstrated by the method set forth by Parker et al in the European Journal of Pharmacology, Vol. 31, pp. 29-37 (1975).

One skilled in the art will recognize that in addition to acetone illustrated as a hydroxy group protecting agent for the hydroxyl groups on di ethyl-bis(hydroxymethyl) malonate many other standard hydroxyl protecting groups may be employed in that synthetic scheme. Among these are dihydropyran for the formation of tetrahydropyanyl ethers, and tri-lower alkyl silyl halides for the formation of tri-lower alkyl silyl esters.

Similarly the partial hydrolysis of the hydroxyl protected malonic diester to produce the decarboxylated half ester may be accomplished by any known ester hydrolysis reagent. One skilled in the art will, of course, adjust the conditions according to the hydroxyl protecting group.

Similarly the reduction of the remaining ester group to an alcohol may be accomplished by many methods equivalent to the use of lithium aluminum hydride as illustrated. Some known equivalents are the use of hydrogen adsorbed on known catalysts, borohydride reducing agents, other derivatives of AlH₃ and its complex salts, the borane-dimethyl sulfide adduct employed in the reduction of methane tricarboxylate esters, and Bouveault Blanc type reductions employing an alkali metal dissolving in a lower alkanol.

The requisite removal of the aforementioned hydroxyl group protecting agents may also be accomplished by known methods, for example, acid hydrolysis is suitable for the removal of tetrahydropyranyl ethers, while basic hydrolysis is preferable for tri-lower alkyl silyl ethers.

As used herein and in the appended claims the term "lower alkyl" comprehends a saturated hydrocarbon radical, either straight, branched chain or cyclic having from 1 to 8 carbon atoms. The term "lower alkanol" comprehends a monohydroxyl substituted lower alkyl group. The term "lower alkoxy" comprehends a radical derived from a lower alkanol by removal of the hydroxyl hydrogen.

The following Examples further illustrate the best mode contemplated by the inventor for the practice of his invention.

EXAMPLE 1 2-Hydroxymethyl-1,3-Propanediol from Bis-(hydroxymethyl) Acetaldehyde

To bis-(hydroxymethyl) acetaldehyde (from hydrolysis of its diethyl acetal (23 g) in water (300 ml.) is added PtO₂ (0.3 g) and FeSO₄.7H₂ O (0.02 g). This mixture is shaken with hydrogen at ambient temperature at 50 to 500 psi until the theoretical quantity (0.13 mole) of hydrogen is absorbed. The catalyst is then removed by filtration, the water removed to give a residue. Distillation of the residue gives 2-hydroxymethyl-1,3-propanediol (10.2 g)(74.5%) B.P. 140° C. (0.005 mm), M.P. 60°-62°.

EXAMPLE 2 2,2-Dimethyl-5,5-Dicarbethoxy-1,3-Dioxane

To diethyl-bis-(hydroxymethyl) malonate (50 g) in acetone (50 ml) and benzene (200 ml) is added phosphoric acid (10 g). The mixture is refluxed while stirring and separating water which distills. When water evolution is complete, the reaction mixture is cooled and the organic layer is separated, stirred with solid sodium carbonate (10 g), filtered and evaporated to give the title product (52 g) (87%) n_(D) ²⁶ 1.4412.

EXAMPLE 3 2,2-Dimethyl-5-Carbethoxy-1,3-Dioxane

To a solution of the product of Example 2 (65 g) in dimethyl sulfoxide (65 g) is added sodium chloride (1 g). The mixture is stirred while warming at about 180° C., and water is added in small portions while maintaining the temperature between 170° and 180°. Ethanol and water are evolved and are removed by distillation until about 60 ml of liquid has been collected. The mixture is cooled, ether (200 ml) added, and the mixture partitioned with 3 portions of water (50 ml). The organic phase is dried over sodium sulfate and evaporated to a residue. Distillation of the residue gives the title product (25 g) (57%) B.P. 38° (0.01 mm) n_(D) ²⁶ 1.4400.

EXAMPLE 4 2,2-Dimethyl-5-Hydroxymethyl-1,3-Dioxane

Lithium aluminum hydride (80 g) is stirred in ether (2000 ml) while the product of Example 3 (230 g) in ether (250 ml) is added dropwise. When the addition is complete the mixture is stirred an additional 16 hours. The reaction mixture is decomposed by careful addition of water (80 ml) followed by 15% aqueous sodium hydroxide (80 ml) and additional water (240 ml). The resulting suspension is filtered, the filter cake washed with ethanol and ether and the combined filtrates evaporated to give a residue. Distillation of the residue gives the title product (155 g) (81%) B.P. 75° C. (0.05 mm).

EXAMPLE 5 2-Hydroxymethyl-1,3-Propanediol

The product of Example 4 (14.6 g) is stirred in water (4 ml) containing concentrated hydrochloric acid (1 drop) for about 18 hours. Evaporation of the water gives a solid residue which is recrystallized from acetone to give the title product (9 g) (85%) M.P. 61°-62°.

EXAMPLE 6 2-Hydroxymethyl-1,3-Propanediol From Tricarboethoxy Methane

Tricarboethoxy methane (1 g) in hexane (or dry tetrahydrofuran) (5 ml) is treated with borane-dimethyl sulfide (2 ml). The reaction mixture is stirred 48 hours at 60° C. Methanol (50 ml) is then added dropwise slowly, avoiding excessive gassing. The volatile solvents are removed in vacuo to give a product (0.45 g) (m.p. 56°-60° C.), which after recrystallization from acetone affords the title product (m.p. 62°-63° C.).

EXAMPLE 7 2-Hydroxymethyl-1,3-Propanediol Trinitrate

To a mixture of methylene chloride (150 ml) and 1:1 mixture of anhydrous nitric acid and 30% fuming sulfuric acid (40 ml) carefully stirred at 10° to 15%C is added portionwise 2-hydroxymethyl-1,3-propanediol (7.5 g) while measuring the redox potential of the solution and maintaining it between -0.07 and 0.20 volts. This is conveniently done with an Ingold Redox probe charged with the mixed acid. When the addition is complete the phases are separated, the organic phase washed with water, aqueous sodium bicarbonate and aqueous urea, dried over sodium sulfate and/or molecular sieves and the solvent evaported to give the title product (15 g) m.p. 11°-12° C., D 1.53, n_(D) ²⁹.5 1.4746.

Analysis for C₄ H₇ N₃ O₉ :

Calculated: N 17.43%; Found: N 17.42%.

I. R. Analysis:

λ_(max) ^(film) : 2970, 1640, 1280, 860 cm⁻¹

N. M. R. Analysis:

Signals at: δ=4.56 (doublet, 6H, --CH₂ --ONO₂), ##STR6##

EXAMPLE 8

The volatilities of nitroglycerin (NG), 2-hydroxymethyl-1,3- propanediol trinitrate (TMMTN), and 2,2-di(hydroxymethyl)-1-propanol trinitrate (TMETN) were measured at 5×10⁻⁵ mm Hg and ambient temperature by determining weight decrease of samples of each material. Using the weight loss of nitroglycerin as a standard the results are

    ______________________________________                                                   Relative Weight Loss                                                 ______________________________________                                         NG          1.0                                                                TMETN       0.26                                                               TMMTN       0.16                                                               ______________________________________                                    

EXAMPLE 9

Thermal stabilities of nitroglycerin (NG) 2-hydroxymethyl-1,3-propanediol trinitrate (TMMTN) and 2,2-di-(hydroxymethyl)-1-propanol trinitrate (TMETN) were evaluated by a number of independent methods.

A. NG, TMMTN and TMETN were incorporated into standard KBr infra red pellets and the rate of disappearance of the nitrate ester peaks at 1640, 1280 and 840 cm⁻¹ determined at 100° and 140° C. the absolute and relative rate constants for the decomposition are as follows:

    ______________________________________                                         FIRST ORDER RATE CONSTANT (R) × 10.sup.6 (sec..sup.-1)                   Temp. Nitrate                                                                  °C.                                                                           Ester    Average  1640 cm.sup.-1                                                                         1280 cm.sup.-1                                                                         840 cm.sup.-1                          ______________________________________                                         100   TMMTN    0.15     0.17    0.19    0.09                                   100   NG       0.29     0.37    0.30    0.22                                   140   TMMTN    2.24     2.82    2.65    1.26                                   140   TMETN    1.63     2.01    1.76    1.11                                   140   NG       3.90     4.70    3.85    3.16                                   ______________________________________                                         RELATIVE RATES                                                                 Nitrate Ester    100°                                                                           140°                                            ______________________________________                                         NG               1.00   1.00                                                   TMMTN            0.52   0.57                                                   TMETN            --     0.42                                                   ______________________________________                                    

B. NG, TMMTN and TMETN were subjected to differential scanning calorimetry with the following results.

    ______________________________________                                                     Beginning of                                                                               Peak of                                                Compound    Exotherm (°C.)                                                                      Exotherm (°C.)                                  ______________________________________                                         TMMTN       175         212                                                    TMETN       163         210                                                    NG          168         193                                                    ______________________________________                                    

C. The thermal stabilities as measured by gas evolution of NG, TMMTN and TMETN were measure at 90° C. with the following results:

    ______________________________________                                         Compound     Stability (ml/g/hr.)                                              ______________________________________                                         TMMTN        0.013                                                             TMETN        0.020                                                             NG           0.024                                                             ______________________________________                                    

D. Samples of NG, TMMTN and TMETN were sealed in a closed pressure vessel for 23 hours at 93° C. with the following results.

    ______________________________________                                         Compound     Pressure Generated                                                ______________________________________                                         TMMTN        0                                                                 TMETN        0                                                                 NG           107.8 mm Hg                                                       ______________________________________                                    

EXAMPLE 10

A propellant having the ingredients in the proportions shown is prepared.

    ______________________________________                                                                 Quantity (%)                                           ______________________________________                                         2-hydroxymethyl-1,3-propanediol                                                                          19.989                                               trinitrate                                                                     PCP-260 (hydroxy terminated polycaprolactone,                                                            4.872                                                Union Carbide)                                                                 Desmodur N-100 (Polyfunctional isocyanate based                                                          0.839                                                on hexamethylene diisocyanate,                                                 Mobay)                                                                         4-nitrodiphenylamine      0.25                                                 Carbon Black              1.0                                                  Triphenylbismuth          0.05                                                 HMX (cyclotetramethylene tetranitramine)                                                                 23.00                                                Ammonium Perchlorate (90μ)                                                                            20.00                                                Ammonium Nitrate (200μ)                                                                               30.00                                                ______________________________________                                    

The formulation shows less plasticizer bleeding than a comparable nitroglycerin formulation and enhanced storage stability while exhibiting only a slightly lowered specific impulse.

EXAMPLE 11

To further illustrate the relative performance of 2,2-di-(hydroxymethyl)-1-propanol trinitrate (TMETN) nitroglycerin (NG) and 2-hydroxymethyl-1,3-propanediol trinitrate (TMMTN) plasticized propellants, computer simulations (which are known to have good correlation with actual performance) for the various propellant compositions shown below have been calculated to determine the specific impulse Isp and density (σ) to be expected of such compositions.

    ______________________________________                                         Propellant                                                                     76% Solids, 58% Oxidizer (Ammonium perchlorate (AP) +                          HMX), 18% Al, Plasticizer/Polymer = 4.0/1                                      Plasticizer                                                                               % AP     0         5     10                                         ______________________________________                                         TMMTN      Isp (sec)                                                                               272.1     272.1 271.4                                                 σ(lb/in.sup.3)                                                                    0.0667    0.0668                                                                               0.0669                                     NG         Isp (sec)                                                                               272.9     272.2 271.4                                                 σ(lb/in.sup.3)                                                                    0.0674    0.0675                                                                               0.0675                                     Propellant                                                                     82% Solids, 64% Oxidizer (AP + HMX) remainder as above                         Plasticizer                                                                               % AP     0         5     10                                         ______________________________________                                         TMMTN      Isp (sec)                                                                               273.9     273.3 272.6                                                 σ(lb/in.sup.3)                                                                    0.0682    0.0683                                                                               0.0684                                     NG         Isp (sec)                                                                               274.2     273.4 272.2                                                 σ(lb/in.sup.3)                                                                    0.0687    0.0688                                                                               0.0689                                     ______________________________________                                         Propellant                                                                     78% HMX, PCP/HDI Binder                                                        Plasticizer/Polymer                                                                            3.5/1     4.0/1   4.5/1                                        ______________________________________                                         TMMTN      Isp (sec)                                                                               254.9     256.0 256.8                                                 σ(lb/in.sup.3)                                                                    0.0636    0.0637                                                                               0.0658                                     NG         Isp (sec)                                                                               257.9     259.0 259.9                                                 σ(lb/in.sup.3)                                                                    0.0644    0.0646                                                                               0.0647                                     TMETN      Isp (sec)                                                                               252.1     253.2 254.0                                                 σ(lb/in.sup.3)                                                                    0.0635    0.0636                                                                               0.0637                                     Propellant                                                                     82% HMX, PCP/HDI Binder                                                        TMMTN      Isp (sec)                                                                               256.9     257.7 258.4                                                 σ(lb/in.sup.3)                                                                    0.0645    0.0646                                                                               0.0646                                     NG         Isp (sec)                                                                               259.3     260.2 260.9                                                 σ(lb/in.sup.3)                                                                    0.0651    0.0653                                                                               0.0654                                     TMETN      Isp (sec)                                                                               254.7     255.5 256.2                                                 σ(lb/in.sup.3)                                                                    0.0644    0.0645                                                                               0.0646                                     ______________________________________                                     

The subject matter which applicant regards as his invention is particularly pointed out and destinctively claimed as follows:
 1. A process for the preparation of 2-hydroxymethyl-1, 3-propanediol which comprises the treatment of bis-(hydroxymethyl) acetaldehyde with an aldehyde carbonyl group reducing agent selected from hydrogen adsorbed on a hydrogenation catalyst or an alkali metal dissolving in a lower alkanol.
 2. A process for the preparation of 2-hydroxymethyl-1,3-propanediol which comprises the treatment of bis-(hydroxymethyl)acetaldehyde with an aldehyde carbonyl group reducing agent selected from hydrogen adsorbed on a platinum, rhodium or palladium hydrogenation catalyst, or an alkali metal dissolving in a lower alkanol.
 3. A process as defined in claim 2, wherein the aldehyde carbonyl group reducing agent is hydrogen adsorbed on a platinum hydrogenation catalyst.
 4. A process as defined in claim 2 wherein the aldehyde carbonyl group reducing agent is hydrogen adsorbed on a rhodium hydrogenation catalyst.
 5. A process as defined in claim 2 wherein the aldehyde carbonyl group reducing agent is hydrogen adsorbed on a palladium hydrogenation catalyst.
 6. A process as defined in claim 2 wherein said alkali metal dissolving in a lower alkanol is sodium dissolving in ethanol. 